Process for burning a combustible liquid employing a particulate carbon-coated cellular ceramic nodule

ABSTRACT

A process for the substantially complete combustion of a combustible liquid including the combustion of a layer of the combustible liquid floating on a body of water. Cellular ceramic nodules are prepared by coating uncellulated pellets with a particulate carbonaceous parting agent and cellulating the coated pellets in a rotary furnace or kiln. The cellular ceramic nodules obtained by the above process have a relatively thin coating of the carbonaceous parting agent thereon and a relatively smooth continuous outer skin. A layer of the coated cellular ceramic nodules is formed on the upper surface of the combustible liquid with a substantial number of the nodules in contiguous relation with adjacent nodules in the layer. The upper exposed surfaces of the coated nodules are wetted with the combustible liquid to form a film or layer thereon and the wetted films on the exposed surfaces of the nodules are ignited until combustion is selfsustaining. The combustible liquid films on the exposed upper surfaces of the coated nodules consumed by combustion, are continually replaced with combustible liquid from the bulk of the liquid until substantially all of the combustible liquid is consumed.

United States Patent Johnston 51 May 9,1972

[72] Inventor: William D. Johnston, Pittsburgh, Pa.

[73] Assignee: Pittsburgh Corning Corporation, Pittsburgh, Pa.

[22] Filed: May 19, 1970 [21] Appl. No.: 38,865

[52] US. Cl ..431/7, 431/326, 210/40 [51] Int. Cl ..F23d 3/18 [58] Field of Search ..43l/2,4, 7, 326; 44/51, 3,

[56] References Cited UNITED STATES PATENTS Combating Pollution Created by Oil Spills. Report to the Department of Transportation, U.S. Coast Guard, Arthur D. Little, lnc. June 30,1969, p. 79-- 85, 101- 103. TD 427. P4, L5.

A Status Report on the Use of Chemicals and Other Materials to Treat Oil Spilled on Water. Federal Water Pollution Control Administration, Department of the Interior, by Edison Water Quality Laboratory, Northeast Region, Edison. NJ. March 1969. p. 19- 20.

Primary Examiner-Frederick L. Matteson Assistant Examiner-W. C. Anderson AttorneyStanley J. Price, Jr.

[5 7] ABSTRACT A process for the substantially complete combustion of a combustible liquid including the combustion of a layer of the combustible liquid floating on a body of water. Cellular ceramic nodules are prepared by coating uncellulated pellets with a particulate carbonaceous parting agent and cellulating the coated pellets in a rotary furnace or kiln. The cellular ceramic nodules obtained by the above process have a relatively thin coating of the carbonaceous parting agent thereon and a relatively smooth continuous outer skin. A layer of the coated cellular ceramic nodules is formed on the upper surface of the combustible liquid with a substantial number of the nodules in contiguous relation with adjacent nodules in the layer. The upper exposed surfaces of the coated nodules are wetted with the combustible liquid to form a film or layer thereon and the wetted films on the exposed surfaces of the nodules are ignited until combustion is self-sustaining. The combustible liquid films on the exposed upper surfaces of the coated nodules consumed by combustion, are continually replaced with combustible liquid from the bulk of the liquid until substantially all of the combustible liquid is consumed.

8 Claims, No Drawings PROCESS FOR BURNING A COMBUSTIBLE LIQUID EMPLOYING A PARTICULATE CARBON-COATED CELLULAR CERAMIC NODULE BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to a process for the burning of a combustible liquid and more particularly to a process for the complete combustion of a layer of combustible liquid floating on a body of water.

2. Description of the Prior Art During the transfer of liquid fuel from one vessel to another, either at sea or on other navigable waters, discharge of combustible hydrocarbon liquids or other pollutants onto the water often occurs. Similarly, accidents in the production and transportation of petroleum products, such as weld blowouts and pipeline leaks, cause major water pollution problems. Such accidents and other catastrophes, such as the sinking or damaging of an ocean going or river transportation vessel, cause water pollution problems that are often unsolvable or that are remedial only at exorbitant expense. The possibility of such incidents of water pollution and contamination of adjacent land areas has severely restricted the recovery of large amounts of petroleum from off-shore reservoirs.

An inexpensive solution would be the combustion of the layer of pollutant liquid from the surface of the water. This solution, however, has not been found feasible for many reasons. For example, many hydrocarbon liquids and other pollutant liquids are not readily ignitable. Furthermore, in many instances in which ignition can be obtained, it is not possible to sustain combustion long enough or at sufficiently high temperatures, to consume the pollutant liquid.

Even when dealing with liquids that ordinarily are readily ignitable and relatively combustible, the presence of a relatively thin layer of such liquid underlain by a large body of water produces a physical system in which ignition cannot be obtained or in which combustion cannot be sustained at all or cannot be sustained at sufficiently high temperatures to efi'ect removal of the pollutant liquid. These problems generally arise from the rapid transfer of heat into the underlying body of water and away from the combustible liquid.

Several other solutions to the pollution problem have been suggested in the prior art. It has been suggested that the pollutant be confined with a ring of trash booms or similar devices and then scooped from the water's surface. That solution has been proved to be exorbitantly time consuming and expensive and not completely effective.

Attempts have also been made to absorb the pollutant liquid in straw or other absorbent material which is subsequently transported from the scene and destroyed. That solution has also proved too expensive, time consuming and not entirely satisfactory.

Another proposed solution to the problem is disclosed in U.S. Pat. No. 3,556,698 and comprises covering the surface of the pollutant liquid with particulate silica particles which have been coated with a surface active agent to render the silica particle hydrophobic and burning the pollutant liquid treated with the silica particles. One problem inherent in he use of this method arises from the fact that not all of the pollutant liquid is consumed and the residue agglomerates with the silica particles leaving crusty patches of siliceous pollutant residue floating on the waters surface. The pollutant residue must be scooped or otherwise removed from the surface.

In reference to the combustion of the pollutant liquid on he surface of the water, attempts have been made to burn away the pollutant liquid through the use of various igniters or combustion catalysts. This method has, in the past, proved unsatisfactory because of the inherent expense and the inability to completely consume and remove the pollutant liquid. The

removal of the pollutant liquid by combustion can be effectively accomplished by a process described and claimed in copending application Ser. No. 829,746, entitled process For Burning a Combustible Liquid Using Cellular Ceramic Nodules", filed on June 2, 1969 and includes floating a layer of cellular ceramic nodules with a textured outer surface on the upper surface of the pollutant liquid and then buming the pollutant-liquid. The cellular ceramic nodules, with the textured outer surface, serve as a combustion enhancing agent so that the layer of pollutant liquid which, without nodules, does not sustain combustion, and with the layer of nodules thereon, bums readily and substantially completely. As described in copending application Ser. No. 829,746, entitled Process For Burning a Combustible Liquid Using Cellular Ceramic Nodules" in the names of Nicholas T. Catellucci and Ned C. Krouskop as applicants, the cellular ceramic nodules are abraded to remove the outer continuous skin and expose the inner surfaces of the separate cells therebeneath and provide the textured outer surface. The removal of V the continuous outer skin by abrasion, is a relatively expensive and time consuming process. Also, the'removal of the outer continuous skin provides a more friable outer surface that requires special handling to prevent degradation and the formation of dust. it has been found that the presence of dust on the nodules surface, adversely affects the efficiency of the nodules as a combustion enhancing agent.

SUMMARY OF THE INVENTION The present invention is an improvement of the process described and claimed in copending application Ser. No. 829,746. Pellets of particulate ceramic material and a cellulating agent are coated with a particulate carbonaceous parting agent and cellulated in a rotary furnace. The cellular ceramic nodules have a thin coating of particulate carbonaceous parting agent adhering to the relatively smooth continuous outer skin. The substantially continuous outer skin provides integrity for the coated nodule so that the surface is not as friable as a nodule with a textured outer surface.

A plurality of the coated cellular ceramic nodules are deposited on the upper surface of the combustible liquid to be burned so that they float thereon with a substantial number of nodules in contiguous relation. The nodules are wetted by the combustible liquid and then the liquid is ignited and burned on the exposed upper surface of the nodules remote from the major portion of the layer of liquid being burned. Combustion of the liquid on the exposed upper surface of the nodule is thereafter continued in a substantially self-sustaining manner until substantially all of the combustible liquid has been bumed'or consumed in the combustion process.

The process includes isolating a portion of the combustible liquid as a film on the exposed surface of the nodules so that the film of combustible liquid is separated from the body of water. On the upper exposed surface of the nodule, remote from the body of water, ignition and sustained combustion of the liquid film takes place. The film of combustible liquid on the upper surface of the nodule is continually replaced with liquid from the layer of combustible liquid through capillary action.

Accordingly, it is an object of this invention to provide a process for substantially completely burning a liquid pollutant and thereby removing the liquid pollutant from the surface of a body of-water. 7

Another object of this invention is to provide a process for enabling or enhancing the combustion of a combustible liquid which is otherwise difficult to ignite or difficult to sustain combustion.

DESCRIPTION OF THE PREFERRED EMBODIMENT Coated cellular ceramic nodules suitable for usein the hereinafter described process may be prepared in a manner similar to the process described in U.S. Pat. No. 3,354,024

ing relatively fine pulverulent glass with acellulating agent such as carbon black, or the like. A binder is then added to the mixture and the mixture is pelletized. The pellets are then coated with a particulate carbonaceous parting agent such as graphite. It has been found that one part by weight of carbonaceous parting agent for each parts by weight of pellets is sufficient to prevent the pellets from sticking and maintains the pellets discrete during the cellulation process. The coated pellets are heated in a rotary furnace or kiln in a reducing atmosphere to a cellulating temperature. The pellets cellulate to form substantially spherical cellular ceramic nodules with a continuous, thin, relatively smooth outer skin coated with a relatively thin layer of the particulate carbonaceous parting agent.

Although pulverulent glass is a preferred constituent of the cellular ceramic nodule, other glassy materials, as described in U.S. Pat. No. 3,441,396 may be used. The term ceramic is intended to encompass both pulverulent formulated glass and other suitable pulverulent glassy materials and clays. The cellular ceramic nodules thus produced have a core of individual, completely closed cells of ceramic material and a substantially continuous relatively smooth thin outer skin of ceramic material with a coating of particulate carbonaceous parting agent adhering thereto.

The process for removing liquid combustible pollutants from a body of water and for enabling and enhancing the combustion of liquids generally includes depositing a quantity of cellular ceramic nodules coated as above described, on the upper free surface of the combustible liquid. The nodules appear to be wetted with the combustible liquid so that thin films of the combustible liquid are isolated from the body of water and supported on the upper exposed portion of the nodules, The film of combustible liquid supported by the coated cellular ceramic nodules readily ignites and burns. Further, the .liquid in the film is continually replaced by other liquid from the layer floating on the body of water. The replacement of the film and combustion continue until substantially all of the combustible liquid floating on the body of water is removed by combustion.

The coated cellular ceramic nodules produced as described above exhibit many characteristics which are readily and preferantially adaptable for the herein described process. For example, in this process the combustion enhancing agent should be impervious or impermeable to the flow of fluids into and through the combustion enhancing agent. Therefore, all of the liquid to be burned remains on the surface of'the combustion enhancing agent and is accessible for combustion and ultimate burning. The combustion enhancing agent remaining after combustion of the combustible liquid is substantially de' void of the combustible liquid, thereby obviating further treatment or purification of the combustion enhancing agent.

The coated cellular ceramic nodules have a density less than the density of the water and preferably less than the density of the liquid to be burned. It is essential that the nodules float on the upper surface of the water and preferably on the upper free surface of the liquid to be burned. It is also preferred that the nodules float on the liquid to be burned with only a portion of the nodule submerged below the surface of the liquid to be burned and have an upper exposed portion above the surface. Nodules produced as previously described generally have an apparent density of between about 6 pounds per cubic foot and 30 pounds per cubic foot. Nodules with a density of the above range have exhibited a high degree of efiiciency when used in this process.

Another preferred property of the combustion enhancing agent is that the agent have a chemical composition that is inert and unreactive with the material to be burned as well as with the surrounding atmosphere and the body of water on which it floats. The coated cellular ceramic nodule is chemically inert with respect to combustible liquid hydrocarbons, air and water so that the surface morphology of the nodule will not be altered substantiallyduring the combustion process and the density and other desirable properties of the nodule will not be altered substantially during the combustion of the combustible liquid thereon.

It is preferred that the gross configuration of the nodule be substantially spherical to provide greater burning efficiency when in contiguous relation. However, the process can be practiced even with an inventory of nodules that exhibit a substantial degree of nonsphericity.

The size of the cellular ceramic nodule is a function of several parameters, among which are the nature of the liquid to be burned; the specific composition and unique morphology of the coated'cellular ceramic nodule employed; the cell size of the nodule; nodule; the ambient physical conditions around the system comprising the nodule; the combustible liquid to be burned, and the underlying water; and the, temperature and other physical and chemical characteristics internal to the system comprising the nodules and the two liquids. In some relatively common circumstances nodules having a diameter of between about one thirty-second inch and one-half inch were found suitable for use in this process. In use with common crude oil and other petroleum products, nodulesv having a diameter of about one-fourth inch were found to be highly effective for use in this process.

It is believed that the thennal properties of the coated cellular ceramic nodules contribute substantially to the combustion process. The efficiency of combustion and of liquid removal are substantially enhanced where the combustion enhancing agent operates in the physical system as a thermal insulator between the body of water and the filin of combustible liquid on the surface of the nodule. The nodules used in this process have a thermal conductivity substantially lower than the combustible liquid. With crude petroleum, other common petroleum products and other hydrocarbon liquids, nodules having a thermal conductivity of between about 0.40 and 0.50

Btu./hr./sq. ft./ F./in. at F. function extremely efficiently and result in the complete combustion and removal of the combustible liquid with no residue remaining in the system.

To maintain a continued burning efficiency, it is also desirable that the melting point of the nodules be substantially higher than the flash point and combustion temperature of the combustible liquid. The coated cellular ceramic nodules produced according to the above described process maintain their physical integrity and surface morphology up to temperatures of about l,000 F. The use of nodules having a high melting point is also desirable because it is believed the herein described process has been found to enhance both the temperature and the rate of combustionfor a given combustible liquid. t

It appears, as the nodules float in the liquid to be burned, that the liquid is lifted from the layer in two ways. First, the liquid forms a thin film around the exposed outer surface of each cellular ceramic nodule and that film is maintained in place by the attractive or adhesive forces generated by the intermolecular forces and attractions between the molecules of the liquid and the coated cellular ceramic nodules. Secondly,

it is believed that a surface capillarityon the surface of the nodule takes place in that preferentially the film of combustible liquid rises onto the exposed nodule surface from the surrounding layer of combustible liquid and the film is continually replaced from the layer by this surface capillarity.

Because of the formation of the thin film of liquid around each nodule and the continued replacement of the liquid, the process functions efficiently with a monolayer, or partial monolayer, of coated cellular ceramic nodules positioned on the surface of the combustible liquid.

A partial monolayer is formed on the surface of the combustible liquid by the self-attraction of the nodules for each other. The nodules have been observed moving toward each other over limited distances into contiguous relation with adjacent nodules and remaining in contiguous relation as'an isolated patch or floating island of nodules. It is believed that the attractive force is created by capillary attraction. A miniscus is formed at each nodule and the nodules are wetted and attracted to each other. Once a floating nodule contacts an adjacent nodule, it has a tendency to adhere thereto. This feature, in addition to contributing to the burning efficiency, is also advantageous when waves are present on the surface of the combustible liquid.

The ignition and combustion of the'combustible liquid is sustained in a combustion zone which may be defined as the upper or exposed surface of the coated cellular ceramic nodules remote from the underlying body of water. In most instances, the creation of the thin film of liquid permits ignition of the liquid by the mere application of heat by means of an open flame on the upper surface of the nodules. In some circumstances, however, where the combustible liquid is not readily ignitable, an igniter such as a highly flammable fluid which has a relatively low flash point can be added to the combustible liquid to facilitate ignition of the combustible liquid. It should be noted, however, that only a relatively small amount of the igniter need be added to the combustible liquid to initiate ignition. After ignition is initiated there is a flame spread across the other nodules in the layer to propagate combustion throughout the entire layer of nodules.

During combustion the amount of liquid supplied to the combustion zone, that is the upper surface of the treated cellular ceramic nodules is, in this process, optimized in the sense that sufficient liquid is supplied to the combustion zone to support rapid, high temperature combustion while excess combustible liquid is maintained below or out of the combustion zone, thereby preventing the wasteful transfer of heat through the combustible liquid to portions of that liquid not being burned in the combustion zone. In addition, the zone of combustion is maintained at the upper surface of the coated cellular ceramic nodules which have the previously discussed thermal insulating properties, thereby separating the heat source from the underlying water and minimizing the heat loss to the body of water therebelow.

With their low thermal conductivity, the nodules function as thermal insulators during combustion thereby preventing loss of heat to the underlying water and confining and concentrat ing the available heat to the region of combustion in the thin film of liquid on the surface of the nodules.

The creation and maintenance of a restricted and insulated combustion zone with a continuous supply of combustible material provides a highly efficient thermal system effecting complete combustion of the liquid at unusually high temperatures and rapid combustion rates. The observed combustion obtained with this process leaves substantially no residue on the surface of the water other than the nodules and provides less noxious fumes and smoke.

The impervious nature of the coated cellular ceramic nodules prevents the absorption of liquid into the nodules themselves with the result that all of the liquid is maintained available for combustion and the surface of the nodules remain substantially unchanged throughout the process to provide a relatively fixed combustion zone.

A substantially spherical shape of the nodules is preferred in their use in this process because the spherical characteristic provides only point contact between contiguous nodules so as not to interfere substantially with capillary spaces between the nodules. It is also believed that the surface morphology of a spherical nodule contributes substantially to the film formation of the combustible liquid previously discussed.

In certain circumstances, such as on a large body of water, it is not always possible to completely cover the surface of the combustible liquid with a layer of coated cellular ceramic nodules. It appears, however, that the nodules are attracted to each other and an isolated monolayer or island of contiguous nodules is formed on a portion of the surface of the liquid and continuous combustion takes place on the floating island of contiguous nodules. Also, during the combustion process, it appears that the combustible liquid is drawn into the area of the isolated island of nodules and upwardly into the combustion zone by the kinetic effects of combustion and the intermolecular cohesion between the liquid molecules and adhesion between the liquid molecules and the coated cellular ceramic nodule. Where necessary, the process can be performed over successive areas of the body of water by confining the combustion process within a suitable boundary element such as a floating ceramic or insulated metal container or fence.

As illustrated in the following Table, the wetting rates of crude oil on the coated nodules were conducted at room temperature and the calculation of these wetting rates were based on the surface area of the spheres and the time for complete wetting. The wetting rate of the coated nodules was compared with that of nodules having particulate alumina parting agent adhering to the outer surface and to the abraded nodules having an abraded textured outer surface. The wetting rates are set forth in Table l.

TABLE I Wetting Rates of Nodules in Crude Oil at Room Temperature (Figures are in mm lmin.)

As is apparent from the above Table l, the wetting rate of the coated nodules is far greater than that for nodules having an abraded or textured surface of nodules have a coating of particulate alumina parting agent adhering thereto.

EXAMPLES Carbon coated nodules were prepared in a manner similar to that previously described in that the pellets were coated with a carbonaceos parting agent and cellulated in a rotary furnace. The carbonaceous parting agent was graphite powder sold by the Acheson Colloids Company of Asbury, NJ. and designated as Grade No. 38 graphite. The particle size of the graphite was such that it passed through a 270 mesh Tyler Standard Screen. Approximately twice as much graphite was employed when compared with the conventional hydrated alumina parting agent. The usual weight ratio of the pellet to the hydrated alumina to maintain the pellets discrete during cellulation is about 20 parts by weight pellets to one part by weight hydrated alumina. A weight ratio of about 10 parts by weight pellets to one part by weight graphite was found to be suitable to maintain the pellets discrete during cellulation. The cellular ceramic nodules cellulated in the presence of the carbonaceous cellulating agent appear to have a relatively smooth, continuous outer surface of skin and a thin coating of the carbonaceous parting agent remains on the surface of the nodule after cellulation. The carbonaceous coating is relatively difficult to remove from the surface of the nodule, even after extensive washing, and the carbon coating appears to have an affinity for the surface of the nodule. The nodules made with the carbonaceous parting agent had a density of about 15 pounds per cubic foot and a size that would pass through an 8 mesh Tyler Standard Screen and be retained on a 12 mesh Tyler Standard Screen.

A series of tests were conducted with Bunker C oil to determine whether the coated nodules were an equivalent combustion enhancing material to nodules with a textured outer surface.

The tests were conducted under the following conditions. A rectangular skirt of aluminum foil having dimensions of about 8 X 8 feet, was weighed. A segment of aluminum foil approximately8 X 8 feet, was weighed. A segment of aluminum foil approximately 72 inches long and 9 inches wide was also weighed. A quart of Bunker C oil was weighed and the coated nodules used in the burn were also weighed. A cylindrical container having a diameter of approximately 22 inches and a height of about l2 inches was positioned on the center of the skirt and filled to within one-fourth inch of the upper rim with water. The strip of aluminum foil was positioned around the container adjacent the upper surface and bent over the annular rim. The weighed quart of oil was then poured on the upper surface of the water in the container and the weighed quantity of coated nodules was positioned on the layer of oil, forming a monolayer of contiguous nodules. After the nodules were wetted by the oil, the oil films on the coated nodules were ignited and the oil burned on the surface of the water. After combustion was complete, a fine mesh colander was weighed and used to remove both the nodules and the remaining oil residue floating on the upper surface of the water. The nodules, residue, colander and the aluminum foil skirt and rim were then placed in an oven and dried until a constant weight was attained. From the above weights, the remaining oil residue after combustion was calculated. I

As a control, dusty, abraded nodules with an inferior surface morphology having a size to pass through a 4 mesh Tyler Standard Screen and being retained on an 8 mesh Tyler Standard Screen were used. The coated nodules had substantially the same size as the control nodules. Nodules having a size capable of passing through a 3' mesh Tyler Standard Screen and being retained on a 6 mesh Tyler Standard Screen with a relatively fine cell size and abraded in a fluidized bed were tested under the above conditions to determine the amount of oil residue remaining after combustion. Further, similar nodules abraded in a ball mill and having substantially the same size as the nodules abraded in a fluidized bed were tested under the above conditions to also determine the efficiency of the nodules as combustion enhancing agents by determining the amountof oil residue remaining after combustion. Table II below enumerates the per cent by weight of the residue or unburned oil remaining after being subjected to combustion with coated nodules, abraded control nodules and nodules abraded in a fluidized bed and in a ball mill.

TABLE I1 by Weight Oil Type of Nodule Residue Remaining Carbon Coated 9.7 fluidized Bed Abraded l [.1 Ball Mill Abraded [1.6 Control 20.1

cially when floating on a body of water.

Although the tests are directed to combustion of Bunker C oil floating on a body of water, it should be understood that it is also possible, with the coated nodules, to obtain controlled combustion of the difficult to ignite petroleum fractions in containers such as pot-like furnaces or the like whereby the carbon coated nodules floating on a body of the liquid isolates a portion of the liquid as a film upon the upper surface of the nodules and the film may be ignited and burned at a controlled rate. The coated nodules may thus be employed to burn the Bunker C oil without air unjection jets, steam jets or chemical treatment of the Bunker C oil.

According to the provisions of the patent statutes, 1 have explained the principle, preferred construction and mode of operation of my invention and what at is now considered to represent its best embodiment has been illustrated and described. However, it should be understood that, within the scope of the appended claims, the invention may be practiced otherwise than as specifically illustrated and described.

I claim: l. A process for burning a combustible liquid comprising, obtaining cellular ceramic nodules having a continuous relatively smooth outer skin with a relatively thin coating of a carbonaceous parting agent adhering thereto,

depositing said nodules with said carbonaceous parting agent adhering to said outer skin on the upper surface of a body of combustible liquid in a manner that said nodules float on said body of combustible liquid and the upper portion of said nodules is exposed above the upper surface of said body of combustible liquid, said cellular ceramic nodules having said coating of carbonaceous parting. agent adhering thereto being impervious to the flow of combustible liquid into and through said nodules,

forming relatively thin films of said combustible liquid on the outer surface of the upper exposed portions of said nodules,

said cellular ceramic nodules having said coating of carbonaceous parting agent adhering thereto insulating said thin films on the outer surface of the upper exposed portions of said nodules from said body of combustible liquid,

igniting and burning said combustible liquid in said thin film, and

continuously replacing said combustible liquid in said thin film from said body of combustible liquid.

2. A process for burning a combustible-liquid as set forth in claim 1 in which,

said carbonaceous parting agent consists of graphite.

3. A process for burning a combustible liquid as set forth in claim 1 in which, 7 i

said carbonaceous parting agent has a size capable of passing through a 270 mesh Tyler Standard Screen.

4. A process for burning a combustible liquid as set forth in claim 1 in which,

said body of combustible liquid comprises a layer floating on the upper surface of a body of water, and

said treated nodules insulating said film from said body of water.

5. A process for burning a combustible liquid as set forth in claim 1 which includes,

forming a monolayer of said treated nodules on the upper surface of said body of combustible liquid, a substantial portion of said coated nodules being in contiguous relation with adjacent nodules.

6. A process for burning a combustible liquid as set forth in claim 1 which includes,

maintaining a portion of said nodules in contact with said layer of combustible liquid,

wetting the exposed upper surface of said nodules with said combustible liquid.

7. A process for burning a combustible liquid as set forth in claim 1 in which,

said nodules have an apparent density of between about 6 and 30 pounds per cubic foot and a thermal conductivity of between about 40 and 50 Btu/hr./sq.ft./ F./in. at 75 F.

8. A process for burning a combustible liquid as set forth in claim 1 in which said treated nodules have a substantially spherical configuration, and

said nodules have a diameter of between about one thirtysecond inch and one-half inch, said treated nodules being impervious to said combustible liquid and chemically inert to said combustible liquid.

I i I 

2. A process for burning a combustible liquid as set forth in claim 1 in which, said carbonaceous parting agent consists of graphite.
 3. A process for burning a combustible liquid as set forth in claim 1 in which, said carbonaceous parting agent has a size capable of passing through a 270 mesh Tyler Standard Screen.
 4. A process for burning a combustible liquid as set forth in claim 1 in which, said body of combustible liquid comprises a layer floating on the upper surface of a body of water, and said treated nodules insulating said film from said body of water.
 5. A process for burning a combustible liquid as set forth in claim 1 which includes, forming a monolayer of said treated nodules on the upper surface of said body of combustible liquid, a substantial portion of said coated nodules being in contiguous relation with adjacent nodules.
 6. A process for burning a combustible liquid as set forth in claim 1 which includes, maintaining a portion of said nodules in contact with said layer of combustible liquid, wetting the exposed upper surface of said nodules with said combustible liquid.
 7. A process for burning a combustible liquid as set forth in claim 1 in which, said nodules have an apparent density of between about 6 and 30 pounds per cubic foot and a thermal conductivity of between about 40 and 50 Btu/hr./sq.ft./* F./in. at 75* F.
 8. A process for burning a combustible liquid as set forth in claim 1 in which said treated nodules have a substantially spherical configuration, and said nodules have a diameter of between about one thirty-second inch and one-half inch, said treated nodules being impervious to said combustible liquid and chemically inert to said combustible liquid. 